CN115259660A - Glass substrate - Google Patents
Glass substrate Download PDFInfo
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- CN115259660A CN115259660A CN202210983759.0A CN202210983759A CN115259660A CN 115259660 A CN115259660 A CN 115259660A CN 202210983759 A CN202210983759 A CN 202210983759A CN 115259660 A CN115259660 A CN 115259660A
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- 239000011521 glass Substances 0.000 title claims abstract description 138
- 239000000758 substrate Substances 0.000 title claims abstract description 91
- 239000000203 mixture Substances 0.000 claims description 17
- 238000000137 annealing Methods 0.000 claims description 7
- 229910018072 Al 2 O 3 Inorganic materials 0.000 claims description 5
- 229910004298 SiO 2 Inorganic materials 0.000 claims description 4
- 239000007791 liquid phase Substances 0.000 claims description 4
- 229910018068 Li 2 O Inorganic materials 0.000 claims description 3
- 229910052785 arsenic Inorganic materials 0.000 claims description 3
- 150000001875 compounds Chemical class 0.000 claims 1
- 238000010438 heat treatment Methods 0.000 description 41
- 239000006060 molten glass Substances 0.000 description 24
- 238000002844 melting Methods 0.000 description 20
- 230000008018 melting Effects 0.000 description 20
- BASFCYQUMIYNBI-UHFFFAOYSA-N platinum Chemical compound [Pt] BASFCYQUMIYNBI-UHFFFAOYSA-N 0.000 description 17
- 238000000034 method Methods 0.000 description 16
- 238000004031 devitrification Methods 0.000 description 14
- 238000002485 combustion reaction Methods 0.000 description 13
- 230000000694 effects Effects 0.000 description 9
- MCMNRKCIXSYSNV-UHFFFAOYSA-N Zirconium dioxide Chemical compound O=[Zr]=O MCMNRKCIXSYSNV-UHFFFAOYSA-N 0.000 description 8
- 229910052697 platinum Inorganic materials 0.000 description 8
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 description 8
- 239000013078 crystal Substances 0.000 description 7
- 230000007423 decrease Effects 0.000 description 7
- 239000006066 glass batch Substances 0.000 description 7
- 238000004519 manufacturing process Methods 0.000 description 7
- 238000007500 overflow downdraw method Methods 0.000 description 7
- 229910052760 oxygen Inorganic materials 0.000 description 7
- 239000002994 raw material Substances 0.000 description 7
- 239000003513 alkali Substances 0.000 description 6
- 229910052708 sodium Inorganic materials 0.000 description 6
- 238000002834 transmittance Methods 0.000 description 5
- 238000005485 electric heating Methods 0.000 description 4
- 238000002156 mixing Methods 0.000 description 4
- 239000004065 semiconductor Substances 0.000 description 4
- 238000003756 stirring Methods 0.000 description 4
- ZOKXTWBITQBERF-UHFFFAOYSA-N Molybdenum Chemical compound [Mo] ZOKXTWBITQBERF-UHFFFAOYSA-N 0.000 description 3
- 229910006404 SnO 2 Inorganic materials 0.000 description 3
- 229910000272 alkali metal oxide Inorganic materials 0.000 description 3
- 229910000287 alkaline earth metal oxide Inorganic materials 0.000 description 3
- 238000002425 crystallisation Methods 0.000 description 3
- 230000008025 crystallization Effects 0.000 description 3
- 239000002803 fossil fuel Substances 0.000 description 3
- 239000000446 fuel Substances 0.000 description 3
- 229910052750 molybdenum Inorganic materials 0.000 description 3
- 239000011733 molybdenum Substances 0.000 description 3
- 238000000465 moulding Methods 0.000 description 3
- 239000000843 powder Substances 0.000 description 3
- 230000008569 process Effects 0.000 description 3
- 238000005033 Fourier transform infrared spectroscopy Methods 0.000 description 2
- 229910021193 La 2 O 3 Inorganic materials 0.000 description 2
- 230000009471 action Effects 0.000 description 2
- 239000002390 adhesive tape Substances 0.000 description 2
- VSCWAEJMTAWNJL-UHFFFAOYSA-K aluminium trichloride Chemical compound Cl[Al](Cl)Cl VSCWAEJMTAWNJL-UHFFFAOYSA-K 0.000 description 2
- QVGXLLKOCUKJST-UHFFFAOYSA-N atomic oxygen Chemical compound [O] QVGXLLKOCUKJST-UHFFFAOYSA-N 0.000 description 2
- 239000011449 brick Substances 0.000 description 2
- 238000001816 cooling Methods 0.000 description 2
- 239000006059 cover glass Substances 0.000 description 2
- 239000002274 desiccant Substances 0.000 description 2
- 239000010408 film Substances 0.000 description 2
- 239000007789 gas Substances 0.000 description 2
- 239000007788 liquid Substances 0.000 description 2
- 239000004973 liquid crystal related substance Substances 0.000 description 2
- 239000000463 material Substances 0.000 description 2
- 239000001301 oxygen Substances 0.000 description 2
- 239000010948 rhodium Substances 0.000 description 2
- 239000007787 solid Substances 0.000 description 2
- ZOXJGFHDIHLPTG-UHFFFAOYSA-N Boron Chemical compound [B] ZOXJGFHDIHLPTG-UHFFFAOYSA-N 0.000 description 1
- VEXZGXHMUGYJMC-UHFFFAOYSA-M Chloride anion Chemical compound [Cl-] VEXZGXHMUGYJMC-UHFFFAOYSA-M 0.000 description 1
- VYPSYNLAJGMNEJ-UHFFFAOYSA-N Silicium dioxide Chemical compound O=[Si]=O VYPSYNLAJGMNEJ-UHFFFAOYSA-N 0.000 description 1
- 229910010413 TiO 2 Inorganic materials 0.000 description 1
- 238000010521 absorption reaction Methods 0.000 description 1
- 229910052782 aluminium Inorganic materials 0.000 description 1
- 229910021417 amorphous silicon Inorganic materials 0.000 description 1
- 229910052661 anorthite Inorganic materials 0.000 description 1
- 239000012298 atmosphere Substances 0.000 description 1
- 230000008901 benefit Effects 0.000 description 1
- 229910052796 boron Inorganic materials 0.000 description 1
- 230000005587 bubbling Effects 0.000 description 1
- 239000003795 chemical substances by application Substances 0.000 description 1
- 239000008395 clarifying agent Substances 0.000 description 1
- 238000004040 coloring Methods 0.000 description 1
- 230000000052 comparative effect Effects 0.000 description 1
- 238000005260 corrosion Methods 0.000 description 1
- 230000007797 corrosion Effects 0.000 description 1
- 229910052906 cristobalite Inorganic materials 0.000 description 1
- GWWPLLOVYSCJIO-UHFFFAOYSA-N dialuminum;calcium;disilicate Chemical compound [Al+3].[Al+3].[Ca+2].[O-][Si]([O-])([O-])[O-].[O-][Si]([O-])([O-])[O-] GWWPLLOVYSCJIO-UHFFFAOYSA-N 0.000 description 1
- KZHJGOXRZJKJNY-UHFFFAOYSA-N dioxosilane;oxo(oxoalumanyloxy)alumane Chemical compound O=[Si]=O.O=[Si]=O.O=[Al]O[Al]=O.O=[Al]O[Al]=O.O=[Al]O[Al]=O KZHJGOXRZJKJNY-UHFFFAOYSA-N 0.000 description 1
- 230000007613 environmental effect Effects 0.000 description 1
- 238000002474 experimental method Methods 0.000 description 1
- 239000006025 fining agent Substances 0.000 description 1
- 239000000295 fuel oil Substances 0.000 description 1
- 125000002887 hydroxy group Chemical group [H]O* 0.000 description 1
- 238000003384 imaging method Methods 0.000 description 1
- 239000012535 impurity Substances 0.000 description 1
- 230000006698 induction Effects 0.000 description 1
- 239000004615 ingredient Substances 0.000 description 1
- 238000009434 installation Methods 0.000 description 1
- 238000011835 investigation Methods 0.000 description 1
- 150000002500 ions Chemical class 0.000 description 1
- 229910052742 iron Inorganic materials 0.000 description 1
- 238000004898 kneading Methods 0.000 description 1
- 229910052751 metal Inorganic materials 0.000 description 1
- 239000002184 metal Substances 0.000 description 1
- 229910052863 mullite Inorganic materials 0.000 description 1
- 239000002245 particle Substances 0.000 description 1
- 239000012071 phase Substances 0.000 description 1
- 238000005191 phase separation Methods 0.000 description 1
- 238000005498 polishing Methods 0.000 description 1
- 229910021420 polycrystalline silicon Inorganic materials 0.000 description 1
- 229920005591 polysilicon Polymers 0.000 description 1
- 239000002244 precipitate Substances 0.000 description 1
- 230000009467 reduction Effects 0.000 description 1
- 238000007670 refining Methods 0.000 description 1
- 229910052703 rhodium Inorganic materials 0.000 description 1
- MHOVAHRLVXNVSD-UHFFFAOYSA-N rhodium atom Chemical compound [Rh] MHOVAHRLVXNVSD-UHFFFAOYSA-N 0.000 description 1
- -1 specifically Substances 0.000 description 1
- 229910001631 strontium chloride Inorganic materials 0.000 description 1
- AHBGXTDRMVNFER-UHFFFAOYSA-L strontium dichloride Chemical compound [Cl-].[Cl-].[Sr+2] AHBGXTDRMVNFER-UHFFFAOYSA-L 0.000 description 1
- 229910052917 strontium silicate Inorganic materials 0.000 description 1
- QSQXISIULMTHLV-UHFFFAOYSA-N strontium;dioxido(oxo)silane Chemical compound [Sr+2].[O-][Si]([O-])=O QSQXISIULMTHLV-UHFFFAOYSA-N 0.000 description 1
- 239000010409 thin film Substances 0.000 description 1
- XOLBLPGZBRYERU-UHFFFAOYSA-N tin dioxide Chemical compound O=[Sn]=O XOLBLPGZBRYERU-UHFFFAOYSA-N 0.000 description 1
- 229910001887 tin oxide Inorganic materials 0.000 description 1
- 229910052845 zircon Inorganic materials 0.000 description 1
- GFQYVLUOOAAOGM-UHFFFAOYSA-N zirconium(iv) silicate Chemical compound [Zr+4].[O-][Si]([O-])([O-])[O-] GFQYVLUOOAAOGM-UHFFFAOYSA-N 0.000 description 1
Images
Classifications
-
- C—CHEMISTRY; METALLURGY
- C03—GLASS; MINERAL OR SLAG WOOL
- C03C—CHEMICAL COMPOSITION OF GLASSES, GLAZES OR VITREOUS ENAMELS; SURFACE TREATMENT OF GLASS; SURFACE TREATMENT OF FIBRES OR FILAMENTS MADE FROM GLASS, MINERALS OR SLAGS; JOINING GLASS TO GLASS OR OTHER MATERIALS
- C03C3/00—Glass compositions
- C03C3/04—Glass compositions containing silica
- C03C3/076—Glass compositions containing silica with 40% to 90% silica, by weight
- C03C3/083—Glass compositions containing silica with 40% to 90% silica, by weight containing aluminium oxide or an iron compound
- C03C3/085—Glass compositions containing silica with 40% to 90% silica, by weight containing aluminium oxide or an iron compound containing an oxide of a divalent metal
- C03C3/087—Glass compositions containing silica with 40% to 90% silica, by weight containing aluminium oxide or an iron compound containing an oxide of a divalent metal containing calcium oxide, e.g. common sheet or container glass
-
- C—CHEMISTRY; METALLURGY
- C03—GLASS; MINERAL OR SLAG WOOL
- C03C—CHEMICAL COMPOSITION OF GLASSES, GLAZES OR VITREOUS ENAMELS; SURFACE TREATMENT OF GLASS; SURFACE TREATMENT OF FIBRES OR FILAMENTS MADE FROM GLASS, MINERALS OR SLAGS; JOINING GLASS TO GLASS OR OTHER MATERIALS
- C03C3/00—Glass compositions
- C03C3/04—Glass compositions containing silica
- C03C3/076—Glass compositions containing silica with 40% to 90% silica, by weight
- C03C3/089—Glass compositions containing silica with 40% to 90% silica, by weight containing boron
- C03C3/091—Glass compositions containing silica with 40% to 90% silica, by weight containing boron containing aluminium
-
- C—CHEMISTRY; METALLURGY
- C03—GLASS; MINERAL OR SLAG WOOL
- C03B—MANUFACTURE, SHAPING, OR SUPPLEMENTARY PROCESSES
- C03B15/00—Drawing glass upwardly from the melt
- C03B15/02—Drawing glass sheets
-
- C—CHEMISTRY; METALLURGY
- C03—GLASS; MINERAL OR SLAG WOOL
- C03B—MANUFACTURE, SHAPING, OR SUPPLEMENTARY PROCESSES
- C03B17/00—Forming molten glass by flowing-out, pushing-out, extruding or drawing downwardly or laterally from forming slits or by overflowing over lips
- C03B17/06—Forming glass sheets
-
- C—CHEMISTRY; METALLURGY
- C03—GLASS; MINERAL OR SLAG WOOL
- C03B—MANUFACTURE, SHAPING, OR SUPPLEMENTARY PROCESSES
- C03B5/00—Melting in furnaces; Furnaces so far as specially adapted for glass manufacture
- C03B5/02—Melting in furnaces; Furnaces so far as specially adapted for glass manufacture in electric furnaces, e.g. by dielectric heating
- C03B5/027—Melting in furnaces; Furnaces so far as specially adapted for glass manufacture in electric furnaces, e.g. by dielectric heating by passing an electric current between electrodes immersed in the glass bath, i.e. by direct resistance heating
-
- C—CHEMISTRY; METALLURGY
- C03—GLASS; MINERAL OR SLAG WOOL
- C03C—CHEMICAL COMPOSITION OF GLASSES, GLAZES OR VITREOUS ENAMELS; SURFACE TREATMENT OF GLASS; SURFACE TREATMENT OF FIBRES OR FILAMENTS MADE FROM GLASS, MINERALS OR SLAGS; JOINING GLASS TO GLASS OR OTHER MATERIALS
- C03C1/00—Ingredients generally applicable to manufacture of glasses, glazes, or vitreous enamels
- C03C1/004—Refining agents
-
- C—CHEMISTRY; METALLURGY
- C03—GLASS; MINERAL OR SLAG WOOL
- C03C—CHEMICAL COMPOSITION OF GLASSES, GLAZES OR VITREOUS ENAMELS; SURFACE TREATMENT OF GLASS; SURFACE TREATMENT OF FIBRES OR FILAMENTS MADE FROM GLASS, MINERALS OR SLAGS; JOINING GLASS TO GLASS OR OTHER MATERIALS
- C03C17/00—Surface treatment of glass, not in the form of fibres or filaments, by coating
- C03C17/06—Surface treatment of glass, not in the form of fibres or filaments, by coating with metals
-
- H—ELECTRICITY
- H05—ELECTRIC TECHNIQUES NOT OTHERWISE PROVIDED FOR
- H05B—ELECTRIC HEATING; ELECTRIC LIGHT SOURCES NOT OTHERWISE PROVIDED FOR; CIRCUIT ARRANGEMENTS FOR ELECTRIC LIGHT SOURCES, IN GENERAL
- H05B33/00—Electroluminescent light sources
- H05B33/02—Details
-
- H—ELECTRICITY
- H10—SEMICONDUCTOR DEVICES; ELECTRIC SOLID-STATE DEVICES NOT OTHERWISE PROVIDED FOR
- H10K—ORGANIC ELECTRIC SOLID-STATE DEVICES
- H10K50/00—Organic light-emitting devices
-
- H—ELECTRICITY
- H10—SEMICONDUCTOR DEVICES; ELECTRIC SOLID-STATE DEVICES NOT OTHERWISE PROVIDED FOR
- H10K—ORGANIC ELECTRIC SOLID-STATE DEVICES
- H10K50/00—Organic light-emitting devices
- H10K50/80—Constructional details
-
- C—CHEMISTRY; METALLURGY
- C03—GLASS; MINERAL OR SLAG WOOL
- C03B—MANUFACTURE, SHAPING, OR SUPPLEMENTARY PROCESSES
- C03B5/00—Melting in furnaces; Furnaces so far as specially adapted for glass manufacture
- C03B5/16—Special features of the melting process; Auxiliary means specially adapted for glass-melting furnaces
- C03B5/235—Heating the glass
- C03B5/2353—Heating the glass by combustion with pure oxygen or oxygen-enriched air, e.g. using oxy-fuel burners or oxygen lances
-
- C—CHEMISTRY; METALLURGY
- C03—GLASS; MINERAL OR SLAG WOOL
- C03B—MANUFACTURE, SHAPING, OR SUPPLEMENTARY PROCESSES
- C03B5/00—Melting in furnaces; Furnaces so far as specially adapted for glass manufacture
- C03B5/16—Special features of the melting process; Auxiliary means specially adapted for glass-melting furnaces
- C03B5/42—Details of construction of furnace walls, e.g. to prevent corrosion; Use of materials for furnace walls
- C03B5/43—Use of materials for furnace walls, e.g. fire-bricks
-
- H—ELECTRICITY
- H10—SEMICONDUCTOR DEVICES; ELECTRIC SOLID-STATE DEVICES NOT OTHERWISE PROVIDED FOR
- H10K—ORGANIC ELECTRIC SOLID-STATE DEVICES
- H10K77/00—Constructional details of devices covered by this subclass and not covered by groups H10K10/80, H10K30/80, H10K50/80 or H10K59/80
- H10K77/10—Substrates, e.g. flexible substrates
-
- Y—GENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
- Y02—TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
- Y02P—CLIMATE CHANGE MITIGATION TECHNOLOGIES IN THE PRODUCTION OR PROCESSING OF GOODS
- Y02P40/00—Technologies relating to the processing of minerals
- Y02P40/50—Glass production, e.g. reusing waste heat during processing or shaping
- Y02P40/57—Improving the yield, e-g- reduction of reject rates
Landscapes
- Chemical & Material Sciences (AREA)
- Engineering & Computer Science (AREA)
- Materials Engineering (AREA)
- Organic Chemistry (AREA)
- Chemical Kinetics & Catalysis (AREA)
- Life Sciences & Earth Sciences (AREA)
- General Chemical & Material Sciences (AREA)
- Geochemistry & Mineralogy (AREA)
- Physics & Mathematics (AREA)
- Optics & Photonics (AREA)
- Electrochemistry (AREA)
- Glass Compositions (AREA)
Abstract
The glass substrate of the present invention is characterized by a high temperature viscosity of 10 2.5 The temperature at dPa.s is less than 1650 ℃, and the temperature is measured by Log eta 500 Estimated viscosity Log η at 500 ℃ calculated as =0.167 × Ps-0.015 × Ta-0.062 × Ts-18.5 500 Is 26.0 or more.
Description
The application is divisional application of patent application with application numbers of 201880023944.7, application dates of 2018, 4 months and 12 days and the name of 'glass substrate'.
Technical Field
The present invention relates to a glass substrate, and more particularly to a glass substrate suitable for a substrate of a flat panel display such as a liquid crystal display and an organic EL display.
Background
Organic EL devices such as organic EL displays are thin, excellent in video display, and low in power consumption, and therefore are used for displays of mobile phones and the like.
As a substrate of an organic EL display, a glass substrate is widely used. Glass substrates for this use are those which do not substantially contain alkali metal oxides or which contain a small amount of alkali metal oxides. In other words, the glass substrate for this use uses a low alkali glass. When the low alkali glass is used, alkali ions can be prevented from diffusing into the semiconductor material produced in the heat treatment step.
In recent years, high-definition displays have been required for smart phones and mobile terminals, and LTPS (Low-temperature poly silicon) TFTs and oxide TFTs have been used as semiconductors of Thin Film Transistors (TFTs) for driving.
Disclosure of Invention
Problems to be solved by the invention
The glass substrate for this use requires, for example, the following characteristics (1) and (2).
(1) Thin glass substrates have high productivity, particularly high melting properties and fining properties.
(2) In the manufacture of LTPS TFT and oxide TFT, the heat treatment temperature is higher than that of conventional amorphous Si TFT. Therefore, the heat resistance is higher than that of the conventional one in order to reduce the heat shrinkage of the glass substrate.
However, it is not easy to satisfy the above-mentioned required characteristics (1) and (2). That is, if the heat resistance of the glass substrate is to be improved, productivity (meltability, fining) tends to be reduced, and conversely, if the productivity of the glass substrate is to be improved, the heat resistance tends to be reduced.
The present invention has been made in view of the above circumstances, and an object of the present invention is to provide a glass substrate that can achieve both productivity and heat resistance.
Means for solving the problems
The present inventors have found that the above technical problem can be solved by limiting the viscosity characteristics of the glass substrate to a predetermined range, and have proposed the present invention. The glass substrate of the present invention is characterized by a high temperature viscosity of 10 2.5 The temperature at dPa · s is 1670 ℃ or less, and the estimated viscosity Log η at 500 ℃ calculated by the following formula 1 500 Is 26.0 or more. Here, "10" is 2.5 The temperature "at dPa · s" can be measured by the platinum ball pulling method. "Strain Point", "annealing Point" and "softening Point" refer to compositions based on ASTM C336,The values measured by the method of ASTM C338.
[ formula 1]
Logη 500 =0.167×Ps-0.015×Ta-0.062×Ts-18.5
Ps: strain point (. Degree. C.)
Ta: annealing Point (. Degree.C.)
Ts: softening Point (. Degree. C.)
The heat resistance of a glass substrate has been evaluated by temperatures such as strain point and annealing point which can be measured. However, these temperature ranges are about 200 ℃ higher or higher than the process temperature for manufacturing LTPS · TFTs and oxide TFTs. Therefore, the temperature of the strain point, annealing point, or the like cannot be evaluated accurately.
The present inventors have repeatedly conducted various experiments and, as a result, found that: the estimated viscosity at 500 ℃ close to the process temperature for manufacturing the LTPS TFT or the oxide TFT is calculated, and if this is used as an index of heat resistance, the heat resistance of the glass substrate can be accurately evaluated.
The present inventors have also found that even if the strain point, which is an index of the past, is the same, the heat resistance is greatly different. Table 1 shows the estimated viscosity Log η at 500 deg.C 500 Data relating to heat shrinkage. The glass composition and the strain point Ps are the same for the glass substrate P and the glass substrate Q. As can be seen from Table 1, the estimated viscosity Log η at 500 ℃ of the glass substrate P 500 27.8, a thermal shrinkage of 17.5ppm, and a viscosity Log η estimated at 500 ℃ of the glass substrate Q 500 29.1 and a heat shrinkage of 12.8ppm. In other words, for the glass substrate P and the glass substrate Q, even if the glass composition and the strain point Ps were the same, the thermal shrinkage rates differed by 4.7ppm. Considering that the heat shrinkage ratio of the glass substrate for a high definition display is particularly preferably 18ppm or less, it can be said that the difference of 4.7ppm is very large. Further, the estimated viscosity Log η at 500 ℃ is determined 500 As an index, the difference can be estimated accurately. Here, the "heat shrinkage rate" is a value calculated as follows. First, a linear mark is marked at a predetermined position of a sample, and the sample is folded perpendicularly to the mark and divided into two glass pieces. Then, only one is neededThe glass sheet was subjected to a predetermined heat treatment (heating at 5 ℃ C./min from room temperature, holding at 500 ℃ C. For 1 hour, and cooling at 5 ℃ C./min). Then, the heat-treated glass sheet and the glass sheet which was not heat-treated were aligned and fixed by an adhesive tape T, and then the shift of the mark was measured. The shift of the mark is set to be Delta L, and the length of the sample before heat treatment is set to be L 0 When using Δ L/L 0 The heat shrinkage was calculated by the following formula (unit: ppm).
[ Table 1]
P | Q | |
Ps[℃] | 740 | 740 |
Thermal shrinkage [ ppm ]] | 17.5 | 12.8 |
Log η poise at 500 DEG C] | 27.8 | 29.1 |
Here, in consideration of the above, the estimated viscosity Log η of the glass substrate of the present invention at 500 ℃ is 500 The limit is 26.0 or more. This can improve the heat resistance of the glass substrate.
On the other hand, if the high melting point component is made largeThe amount of the viscosity Log η can be adjusted to 500 ℃ by introducing the amount into the glass composition 500 However, in this case, the meltability and the fining property are reduced, and the productivity of the glass substrate is reduced. Here, the glass substrate of the present invention is obtained by forming a glass substrate having a high-temperature viscosity of 10 2.5 The temperature at dPa · s is limited to 1670 ℃ or less, thereby preventing the above.
In addition, the glass substrate of the present invention preferably has an a value of 25.0 or more, which is calculated by the following formula 2.
[ formula 2]
A value = Log η 500 - [ beta-OH value (mm) -1 )]×[B 2 O 3 (mass%)]
Here, the "β -OH value" is a value calculated from the following formula 3 using FT-IR.
[ formula 3]
beta-OH value = (1/X) log (T) 1 /T 2 )
X: plate thickness (mm)
T 1 : reference wavelength 3846cm -1 Transmittance (%) of
T 2 : hydroxyl absorption wavelength of 3600cm -1 Near minimum transmittance (%)
The glass substrate of the present invention preferably has a β -OH value of 0.20/mm or less.
The glass substrate of the present invention preferably has a β -OH value of 0.15/mm or less.
In addition, the glass substrate of the present invention is preferably B in the glass composition 2 O 3 The content of (B) is less than 2.0 mass%.
The glass substrate of the present invention preferably contains 55 to 65% by mass of SiO as a glass composition 2 16 to 22 percent of Al 2 O 3 0 to 1% of B 2 O 3 0 to less than 0.1% of Li 2 O+Na 2 O+K 2 O, 1 to 6 percent of MgO, 2 to 8 percent of CaO, 0 to 2 percent of SrO, 4 to 13 percent of BaO and 0 to less than 0.010 percent of As 2 O 3 0 to less than 0.010% of Sb 2 O 3 。
In addition, the glass substrate of the present invention is preferably made of glassFe in (B) 2 O 3 The content of (B) is 0.010 mass% or less.
The glass substrate of the present invention preferably has a liquidus temperature of 1300 ℃ or lower. The "liquidus temperature" herein means a temperature at which devitrification (devitrification crystal) is observed in glass when the glass powder remaining in a 50 mesh (300 μm) is put into a platinum boat through a standard sieve of 30 mesh (500 μm), and then held in a temperature gradient furnace for 24 hours, and then the platinum boat is taken out.
The glass substrate of the present invention is preferably formed by an overflow down-draw method, in other words, by having a forming converging surface in the center of the thickness of the glass substrate. Here, the "overflow drawing method" is a method in which: molten glass is caused to overflow from both sides of a heat-resistant chute-like structure, and the overflowing molten glass is caused to merge at the lower end of the chute-like structure and to extend downward to form a glass substrate.
In addition, the glass substrate of the present invention is preferably used for a substrate of an organic EL device.
Drawings
Fig. 1 is data showing a relationship between the a value and the heat shrinkage ratio.
Detailed Description
In the glass substrate of the present invention, the high temperature viscosity is 10 2.5 The temperature at the time of mooring is 1670 ℃ or lower, preferably 1650 ℃ or lower, 1640 ℃ or lower, 1630 ℃ or lower, and particularly preferably 1500 to 1620 ℃. If 10 2.5 When the temperature at the bottom is high, the meltability and the clarity are reduced, and the production cost of the glass substrate increases.
In the glass substrate of the present invention, the estimated viscosity Log η at 500 ℃ is 500 Is 26.0 or more, preferably 28.0 or more, 28.5 or more, 29.0 or more, and particularly preferably 29.5 to 35. If the estimated viscosity Log η at 500 ℃ is 500 If the amount is too low, the heat resistance of the glass substrate decreases, and the thermal shrinkage of the glass substrate increases.
According to the investigation of the present inventors, it was found that the a value = Log η 500 - [ beta-OH value]×(B 2 O 3 Content (b) shows a high correlation with the measured value of the heat shrinkage rate, and when the value a is large, the heat shrinkage rate becomes small. FIG. 1 shows the A value and the heat shrinkageData of the relationship of (a). In the glass substrate of the present invention, the value a is preferably 25.0 or more, 27.0 or more, 28.0 or more, 29.0 or more, and particularly preferably 30.0 to 40.0. If the value a is too small, the heat resistance of the glass substrate is lowered, and the thermal shrinkage rate of the glass substrate is likely to increase.
From the formula 3, it is understood that the water present in a small amount in the glass affects the relaxation behavior of the glass. The relaxation is a rapid relaxation different from a slow relaxation governed by viscosity, and the rate of rapid relaxation gradually increases as the thermal shrinkage rate decreases. This rapid relaxation is likely to occur when the amount of water in the glass increases. Therefore, as the amount of water in the glass is smaller, rapid relaxation is more difficult to occur, and the effect of reducing the thermal shrinkage rate is relatively high in a glass region having a low thermal shrinkage rate as in the glass substrate of the present invention. Therefore, the β -OH value is preferably 0.20/mm or less, 0.15/mm or less, 0.12/mm or less, 0.11/mm or less, 0.10/mm or less, 0.09/mm or less, 0.07/mm or less, and particularly preferably 0.01 to 0.05/mm.
As a method for reducing the β -OH value, there are the following methods (1) to (7), among which the methods (1) to (4) are effective. (1) selecting a raw material with a low water content. (2) Adding Cl and SO into glass batch 3 And the like. And (3) heating by electrifying through the heating electrode. And (4) adopting a small melting furnace. (5) the amount of water in the furnace atmosphere is reduced. (6) N in molten glass 2 And (4) bubbling. (7) increasing the flow rate of the molten glass.
As shown in formula 3, B in the glass composition 2 O 3 The smaller the content of (b), the lower the heat shrinkage ratio. This is because B 2 O 3 The smaller the content of (b), the more easily the state of low moisture content in the glass can be maintained. Specifically, if B 2 O 3 Particularly, if the glass contains a large amount of tridentate boron, the solubility of water increases, and it is difficult to maintain the state where the water content in the glass is low. Therefore, in the glass substrate of the present invention, B in the glass composition 2 O 3 The content of (b) is preferably 2% by mass or less, 1.5% by mass or less, 1% by mass or less, and less than 1.0% by mass, and particularly preferably 0.1 to 0.9% by mass.
Glass of the inventionThe glass substrate preferably contains 55 to 65% by mass of SiO as a glass composition 2 16 to 22% of Al 2 O 3 0 to 1% of B 2 O 3 0 to less than 0.1% of Li 2 O+Na 2 O+K 2 O, 1 to 6 percent of MgO, 2 to 8 percent of CaO, 0 to 2 percent of SrO, 4 to 13 percent of BaO and 0 to less than 0.010 percent of As 2 O 3 0 to less than 0.010% of Sb 2 O 3 . The reason why the contents of the respective components are limited as described above will be described below. In the description of the content of each component,% represents mass%.
SiO 2 The lower limit range of (a) is 55% or more, 56% or more, 57% or more, 58% or more, particularly 59% or more, and the upper limit range of (b) is preferably 65% or less, 64% or less, 63% or less, particularly 62% or less. If SiO 2 If the content of (B) is too small, al-containing particles tend to be formed 2 O 3 The strain point is easily lowered at the same time as devitrification crystallization of (2). On the other hand, if SiO 2 When the content (b) is too large, the high-temperature viscosity increases, the meltability tends to decrease, and devitrified crystals such as cristobalite precipitate, and the liquid phase temperature tends to increase.
Al 2 O 3 The lower limit of the range is 16% or more, 17% or more, 18% or more, particularly 18.5% or more, and the upper limit of the range is 22% or less, 21% or less, particularly 20% or less. If Al is present 2 O 3 When the content of (b) is too small, the strain point is liable to be lowered, and the glass is liable to be phase-separated. On the other hand, if Al 2 O 3 When the content of (b) is too large, devitrification and crystallization of mullite, anorthite, and the like occur, and the liquid phase temperature tends to be high.
Related to B 2 O 3 Suitable amounts of (b) are as described above.
As mentioned above, li 2 O、Na 2 O and K 2 O is a component that deteriorates characteristics of the semiconductor film. Thus, li 2 O、Na 2 O and K 2 The total amount of O and the respective content are preferably less than 1.0%, less than 0.50%, less than 0.20%, less than 0.10%, less than 0.08%, in particular less than 0.06% of the total weight of the composition. On the other hand, if a small amount of Li is introduced 2 O、Na 2 O and K 2 O lowers the resistivity of the molten glass, and the glass is easily melted by the energization and heating by the heating electrode. Thus, li 2 O、Na 2 O and K 2 The total amount and the respective contents of O are preferably 0.01% or more, 0.02% or more, 0.03% or more, 0.04% or more, and particularly 0.05% or more. In consideration of the influence on the semiconductor film and the reduction in resistivity, it is preferable that Li be used 2 O、Na 2 O and K 2 Preferential introduction of Na into O 2 O。
MgO is a component that reduces high-temperature viscosity and improves meltability. The MgO content is preferably 1 to 6%, 2 to 5.5%, 2.5 to 5.5%, particularly 3 to 5%. If the content of MgO is too small, the above-described effects are difficult to obtain. On the other hand, if the content of MgO is too large, the strain point tends to decrease.
CaO is a component that reduces the high-temperature viscosity and improves the meltability without lowering the strain point. In addition, caO is a component in which a relatively low-cost raw material is introduced into an alkaline earth metal oxide, thereby reducing the raw material cost. The content of CaO is preferably 2 to 8%, 3 to 8%, 4 to 9%, 4.5 to 8%, particularly 5 to 7%. If the content of CaO is too small, the above-described effects are difficult to obtain. On the other hand, if the content of CaO is too large, the thermal expansion coefficient becomes too high and the glass is liable to devitrify.
SrO is a component for improving resistance to devitrification, and is a component for improving fusibility by reducing high-temperature viscosity without lowering strain point. The SrO content is preferably 0 to 2%, 0 to 1.5%, 0.1 to 1.5%, 0.2 to 1%, especially 0.3 to less than 1.0%. If the SrO content is too small, it becomes difficult to obtain the effect of suppressing phase separation and the effect of improving resistance to devitrification. On the other hand, if the SrO content is too large, the compositional balance of the glass composition is lost, and the strontium silicate type devitrified crystal is likely to precipitate.
BaO is a component that significantly improves devitrification resistance among alkaline earth metal oxides. The content of BaO is preferably 4 to 13%, 5 to 12%, 6 to 11%, particularly 7 to 10%. If the content of BaO is too small, the liquidus temperature becomes high and the devitrification resistance is liable to decrease. On the other hand, if the content of BaO is too large, the compositional balance of the glass composition is broken, and devitrified crystals containing BaO are likely to precipitate.
RO (the total amount of MgO, caO, srO and BaO) is preferably 10 to 22%, 13 to 21%, 14 to 20%, particularly 15 to 20%. If the RO content is too small, the meltability tends to be low. On the other hand, if the RO content is too high, the compositional balance of the glass composition is lost, and the devitrification resistance is liable to decrease.
As when the glass is melted by the electric heating of the heating electrode without being heated by the combustion flame of the burner 2 O 3 、Sb 2 O 3 These are components for coloring glass, and the content is preferably less than 0.010%, particularly preferably less than 0.0050%, respectively.
In addition to the above components, for example, the following components may be added to the glass composition. From the viewpoint of reliably obtaining the effects of the present invention, the content of the other components than the above components is preferably 5% or less, and particularly preferably 3% or less, in total.
ZnO is a component for improving meltability, but if ZnO is contained in a large amount, the glass is easily devitrified, and the strain point is easily lowered. The content of ZnO is preferably 0 to 5%, 0 to 3%, 0 to 0.5%, particularly 0 to 0.2%.
P 2 O 5 Is a component for increasing the strain point, but if it contains a large amount of P 2 O 5 The glass is easily phase separated. P 2 O 5 The content of (B) is preferably 0 to 1.5%, 0 to 1.2%, particularly 0 to 1%.
TiO 2 Is a component for lowering high-temperature viscosity and improving meltability, and is a component for suppressing negative induction (solarization), but if a large amount of TiO is contained 2 The glass is colored, and thus the transmittance is easily lowered. Thus, tiO 2 The content of (B) is preferably 0 to 3%, 0 to 1%, 0 to 0.1%, particularly 0 to 0.02%.
Fe 2 O 3 Are inevitably mixed as impurities derived from the glass raw materialThe ingredients are added. In addition, fe 2 O 3 In some cases, the glass is expected to be added positively (for example, 0.003% or more, particularly 0.005% or more) as a refining agent or an effect of lowering the resistivity of molten glass. On the other hand, from the viewpoint of improving the transmittance in the ultraviolet region, it is preferable to reduce Fe as much as possible 2 O 3 The content of (a). When the transmittance in the ultraviolet region is increased, the irradiation efficiency when the laser beam in the ultraviolet region is used in a process related to a display device can be improved. Thus, fe 2 O 3 The content of (b) is preferably 0.020% or less, 0.015% or less, 0.010% or less, and particularly less than 0.010%.
Y 2 O 3 、Nb 2 O 5 、La 2 O 3 Has the effects of improving strain point, young's modulus, etc. However, if the content of these components is too large, the density and the raw material cost are liable to increase. Thus, Y 2 O 3 、Nb 2 O 5 、La 2 O 3 The content of (b) is preferably 0 to 3%, 0 to 1%, 0 to less than 0.10%, and particularly preferably 0 to less than 0.05%, respectively.
Cl is a component that functions as a drying agent and lowers the β -OH value. Therefore, when Cl is introduced, the lower limit content is preferably 0.001% or more, 0.003% or more, and particularly 0.005% or more. However, if the Cl content is too large, the strain point is easily lowered. Therefore, the upper limit content of C1 is preferably 0.5% or less, 0.2% or less, and particularly 0.08% or less. As a raw material for introducing Cl, a chloride of an alkaline earth metal oxide such as strontium chloride, aluminum chloride, or the like can be used.
SO 3 Is a component that functions as a desiccant and reduces the beta-OH value. Therefore, in the introduction of SO 3 In the case of (3), the lower limit content is preferably 0.0001% or more, and more preferably 0.0005% or more. However, if SO 3 If the content of (b) is too large, reboil bubbles are easily generated. Thus, SO 3 The upper limit content of (b) is preferably 0.05% or less, 0.01% or less, 0.005% or less, particularly 0.001% or less.
SnO 2 The component has a good clarifying action in a high temperature region, a high strain point, and a low high temperature viscosity. SnO 2 The content of (b) is preferably 0 to 1%, 0.001 to 1%, 0.05 to 0.5%, and particularly preferably 0.1 to 0.3%. If SnO 2 When the content of (B) is too large, snO 2 Devitrification crystals of (2) are liable to precipitate. If SnO is required 2 If the content of (b) is less than 0.001%, the above-mentioned effects are hardly obtained.
SnO may also be used as long as it does not significantly impair the glass properties 2 Other clarifying agents. Specifically, ceO may be added in a total amount 2 F, C to 1%, for example, and metal powders of Al, si, etc. may be added to 1%, for example, in total.
The glass substrate of the present invention preferably has the following characteristics.
The strain point is preferably 700 ℃ or higher, 720 ℃ or higher, 730 ℃ or higher, 740 ℃ or higher, 750 ℃ or higher, and particularly 760 to 840 ℃. Thus, in the manufacturing process of LTPS TFT and oxide TFT, the heat shrinkage of the glass substrate is easily suppressed.
The liquid phase temperature is preferably 1300 ℃ or lower, 1280 ℃ or lower, 1260 ℃ or lower, 1250 ℃ or lower, and particularly 900 to 1230 ℃. This makes it easy to prevent devitrification crystals from occurring during molding. Further, since the glass substrate is easily formed by the overflow down-draw method, the surface quality of the glass substrate can be improved. The liquidus temperature is an index of resistance to devitrification, and the lower the liquidus temperature, the more excellent the resistance to devitrification.
The viscosity at the liquidus temperature is preferably 10 4.8 Poise above, 10 5.0 Poo Yuan, 10 5.3 Poise or higher, in particular 10 5.5 ~10 7.0 Poise. This makes it easy to prevent devitrification and crystallization from occurring during molding. Further, since the glass substrate is easily formed by the overflow down-draw method, the surface quality of the glass substrate can be improved. The "viscosity at liquidus temperature" can be measured by the platinum ball pulling method.
The heat shrinkage at a temperature rise from room temperature at a rate of 5 ℃/min, holding at 500 ℃ for 1 hour, and a temperature drop at a rate of 5 ℃/min is preferably 21ppm or less, 18ppm or less, 15ppm or less, 12ppm or less, particularly 1 to 10ppm. When the heat shrinkage ratio is large, the production yield of high-definition panels tends to decrease.
In the glass substrate of the present invention, the plate thickness is preferably 0.05 to 0.7mm, 0.1 to 0.5mm, particularly 0.2 to 0.4mm. As the thickness is smaller, the weight and thickness of the display can be reduced more easily. In addition, although the necessity of increasing the forming speed (sheet drawing speed) becomes high when the sheet thickness is small, in this case, the thermal shrinkage of the glass substrate tends to increase, in the present invention, since the heat resistance is high, even if the forming speed (sheet drawing speed) is high, the above can be effectively suppressed.
The glass substrate of the present invention is preferably formed by an overflow down-draw method, in other words, by having a forming converging surface in the center of the thickness of the glass substrate. In the overflow down-draw method, the surface to be the surface of the glass substrate is formed in a free surface state without being in contact with the trough-shaped refractory. Therefore, a glass substrate having good surface quality without polishing can be produced at low cost. In addition, the overflow down-draw method also has such an advantage that a thin glass substrate is easily formed.
The manufacturing process of the glass substrate generally includes: a blending step, a melting step, a clarifying step, a supplying step, a stirring step, and a forming step. The blending step is a step of blending glass raw materials to produce a glass batch. The melting step is a step of obtaining molten glass by melting a batch of glass. The fining step is a step of fining the molten glass obtained in the melting step by the action of a fining agent or the like. The supply step is a step of transferring the molten glass between the steps. The stirring step is a step of stirring and homogenizing the molten glass. The forming step is a step of forming the molten glass into a plate shape. If necessary, a step other than the above-described step, for example, a state adjustment step of adjusting the molten glass to a state suitable for the molding state may be introduced after the stirring step.
Low alkali glass is generally melted by heating by combustion in a burner. The burner is generally disposed above the melting furnace, and fossil fuel, specifically, liquid fuel such as heavy oil, gas fuel such as LPG, or the like is used as fuel. The combustion flame can be obtained by burning a mixed gas of a fossil fuel and oxygen.
However, in the combustion heating by the burner, a large amount of water is mixed into the molten glass, and thus the β — OH value of the glass substrate tends to increase. Therefore, as a method for industrially producing the glass substrate of the present invention, it is preferable to subject a glass batch to electric heating by a heating electrode. In this way, the temperature of the molten glass is lowered from the bottom surface of the melting furnace toward the upper surface of the melting furnace by the energization heating of the heating electrodes provided on the wall surface of the melting furnace, and therefore a large amount of glass batches in a solid state are present on the liquid surface of the molten glass in the melting furnace. As a result, the moisture adhering to the glass batch in a solid state evaporates, and an increase in the amount of moisture due to the raw material can be suppressed. Further, when the heating electrode is used for the electric heating, the energy per unit mass for obtaining the molten glass is reduced, and the amount of the volatile matter to be melted is reduced, so that the environmental load can be reduced.
As a method for industrially producing the glass substrate of the present invention, it is more preferable to perform energization heating by a heating electrode without performing combustion heating by a burner. When the combustion heating is performed by a burner, moisture generated during the combustion of fossil fuel is easily mixed into the molten glass. Therefore, the β -OH value of the molten glass is easily reduced without performing combustion heating by a burner. Note that "the heating electrode performs the energization heating without performing the combustion heating by the burner" means that the glass batch is continuously melted by performing the energization heating only by the heating electrode, but the following cases are excluded: for example, when combustion heating is performed by a burner at the time of starting the melting furnace, combustion heating by the burner is performed locally and secondarily at a specific portion of the melting furnace.
The heating by the heating electrode is preferably performed by applying an ac voltage to the heating electrode provided at the bottom or side of the melting furnace so as to contact the molten glass in the melting furnace. The material for the heating electrode preferably has heat resistance and corrosion resistance against molten glass, and for example, tin oxide, molybdenum, platinum, rhodium, or the like can be used. Molybdenum is particularly preferable because it has high heat resistance and high degree of freedom in installation in a melting furnace.
The low alkali glass has a high specific resistance because of a small content of alkali metal oxide. Therefore, when the electric heating by the heating electrode is applied to the low alkali glass, the electric current flows not only through the molten glass but also through the refractory constituting the melting furnace, and there is a possibility that the refractory is damaged more rapidly. In order to prevent this, as the furnace refractory, a zirconia-based refractory having high resistivity is preferably used, and particularly, a zirconia fused brick is preferable, and as described above, a component (Li) which lowers resistivity is also preferable 2 O、Na 2 O、K 2 O、Fe 2 O 3 Etc.) are introduced into the molten glass in small amounts. ZrO in the zirconia-based refractory 2 The content of (b) is preferably 85% by mass or more, particularly 90% by mass or more.
Examples
The present invention will be described below based on examples. However, the following examples are only illustrative. The present invention is not limited in any way by the following examples.
Table 2 shows examples (sample Nos. 1 to 6) and comparative examples (sample Nos. 7 to 9) of the present invention.
[ Table 2]
First, in order to obtain the glass composition and β — OH value shown in the table, a glass batch after blending was charged into a small-sized test melting furnace constructed of zirconia electrocast bricks, and then, the glass batch was melted at 1600 to 1650 ℃ by energization heating with a molybdenum electrode without heating with a combustion flame of a burner. In samples nos. 1 to 6, the burners were used only when the melting furnace started to operate, and were stopped after molten glass was produced. As to samples No.7 to 9, heating by a combustion flame of an oxygen burner and energization by a heating electrode were simultaneously employedAnd melted by electrical heating. Next, the molten glass was refined and stirred in a Pt — Rh vessel, and then supplied to a zircon forming body, and formed into a flat plate shape having a thickness of 0.5mm by an overflow down-draw method. The resulting glass substrate was evaluated for the beta-OH value, the thermal shrinkage rate, and the estimated viscosity Log eta at 500 ℃ 500 Strain point Ps, annealing point Ta, softening point Ts, 10 4.0 Temperature at viscosity of poise, 10 3.0 Temperature at viscosity of poise, 10 2.5 Temperature at viscosity of poise, liquidus temperature TL, viscosity log η TL at liquidus temperature, and A value.
Estimated viscosity Log η at 500 deg.C 500 Is a value calculated from the above equation 1.
The value a is a value calculated from the above equation 2.
The heat shrinkage ratio is a value calculated as follows. First, a linear mark is marked at a predetermined position of a sample, and the sample is folded perpendicularly to the mark and divided into two glass pieces. Then, only one of the glass sheets was subjected to a predetermined heat treatment (heating at a rate of 5 ℃/min from room temperature, holding at 500 ℃ for 1 hour, and cooling at a rate of 5 ℃/min). Then, the heat-treated glass sheet and the glass sheet which was not heat-treated were aligned and fixed by an adhesive tape T, and then the shift of the mark was measured. The shift of the mark is set to be Delta L, and the length of the sample before heat treatment is set to be L 0 When using Δ L/L 0 The heat shrinkage was calculated by the following formula (unit: ppm).
The β -OH value is a value calculated from the above formula 3 using FT-IR.
The strain point Ps, annealing point Ta, and softening point Ts are values measured by the methods of ASTM C336 and ASTM C338.
The liquidus temperature TL is as follows: the temperature at which crystals precipitated was measured by placing the glass powder remaining in a 50 mesh (300 μm) screen through a standard 30 mesh (500 μm) platinum boat and then holding the boat in a temperature gradient furnace for 24 hours. The viscosity log η TL at the liquidus temperature is a value measured by the platinum ball pulling method.
As is clear from Table 2, the estimated viscosity Log η at 500 ℃ of sample Nos. 1 to 6 500 High and high temperature viscosity 10 2.5 The temperature at the time of the kneading is low, so that the heat shrinkage is small and the productivity is high. On the other hand, sample No.7 had a high-temperature viscosity of 10 2.5 The temperature at the poise is high and therefore the productivity is low. Sample Nos. 8 and 9 had estimated viscosities Log η at 500 ℃ of the respective samples 500 Low, and therefore, large in heat shrinkage.
Industrial applicability
The glass substrate of the present invention is suitable for use as a cover glass for an image sensor such as a Charge Coupled Device (CCD) or a constant contact solid-state imaging device (CIS), a substrate for a solar cell, a cover glass, a substrate for organic EL lighting, and the like, in addition to a substrate for a flat panel display such as a liquid crystal display or an organic EL display.
Claims (10)
1. A glass substrate characterized in that a glass substrate,
high temperature viscosity 10 2.5 The estimated viscosity Log eta at 500 ℃ calculated from the following formula, wherein the temperature at the time of mooring is 1670 ℃ or less 500 The content of the compound is more than 26.0,
Logη 500 =0.167×Ps-0.015×Ta-0.062×Ts-18.5
ps: strain point (. Degree. C.)
Ta: annealing Point (. Degree. C.)
Ts: softening point (. Degree. C.).
2. Glass substrate according to claim 1,
the A value calculated by the following formula is 25.0 or more,
a value = Log η 500 - [ beta-OH value (mm) -1 )]×[B 2 O 3 (mass%)]。
3. Glass substrate according to claim 1 or 2,
the beta-OH value is less than 0.20/mm.
4. Glass substrate according to any one of claims 1 to 3,
the beta-OH value is less than 0.15/mm.
5. Glass substrate according to any one of claims 1 to 4,
B 2 O 3 the content of (B) is less than 2.0 mass%.
6. The glass substrate according to any one of claims 1 to 5,
the glass composition contains 55 to 65 mass% of SiO 2 16 to 22 percent of Al 2 O 3 0 to 1% of B 2 O 3 0 to less than 0.1% of Li 2 O+Na 2 O+K 2 O, 1 to 6 percent of MgO, 2 to 8 percent of CaO, 0 to 2 percent of SrO, 4 to 13 percent of BaO and 0 to less than 0.010 percent of As 2 O 3 0 to less than 0.010% of Sb 2 O 3 。
7. Glass substrate according to any one of claims 1 to 6,
fe in glass composition 2 O 3 The content of (B) is 0.010 mass% or less.
8. Glass substrate according to any one of claims 1 to 7,
the liquid phase temperature is 1300 ℃ or lower.
9. The glass substrate according to any one of claims 1 to 8,
the plate thickness center part has a forming converging surface.
10. The glass substrate according to any one of claims 1 to 9,
the glass substrate is used for a substrate of an organic EL device.
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